Application of James Donald Walker (Two Cases)

324 F.2d 977, 51 C.C.P.A. 954
CourtCourt of Customs and Patent Appeals
DecidedDecember 12, 1963
DocketPatent Appeals 6772, 7058
StatusPublished
Cited by1 cases

This text of 324 F.2d 977 (Application of James Donald Walker (Two Cases)) is published on Counsel Stack Legal Research, covering Court of Customs and Patent Appeals primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Application of James Donald Walker (Two Cases), 324 F.2d 977, 51 C.C.P.A. 954 (ccpa 1963).

Opinion

WORLEY, Chief Judge.

This case involves two consolidated appeals from the Board of Appeals. Patent Appeal No. 6772 is from the board’s affirmance of the examiner’s rejection of claims 24 through 34 and 36 through 39, the only remaining claims in appellant’s application Serial No. 717,681. Patent Appeal No. 7058 is from that part of the board’s decision refusing claims 9 to 12, 23, 24, and 27 through 29 of application Serial No. 511,453, the board having reversed the examiner’s rejection of claims 18, 22, 25, 26 and 32, the remaining claims in that application. Application Serial No. 717,681 is designated by appellant as a “straight continuation” of Serial No. 511, 453 1

*979 The two applications disclose the same subject matter, the aeration of liquids such as sewage by liberating air from spaced clusters of orifices near the bottom of a tank to produce a circulating roll of the contents of the tank. The applications state:

“According to the present invention, efficient aeration is accomplished solely by the supply of air through air orifices large enough not to clog but especially arranged to produce a functioning not previously anticipated. The orifices are provided in clusters well separated from other clusters and near the wall or boundary of the circulating roll desired. A sufficient quantity of air is liberated through them to develop the required circulating roll. As this circulation develops, a stable condition is reached, at which unexpected factors produce efficient aeration. As the air leaves the cluster of orifices, it passes upwardly for a foot or two in a rather compact stream of air bubbles which seem to have a smooth flow action which would make them quite inadequate for aeration. As they rise, however, they encounter critical conditions which rather suddenly convert the smooth-flowing stream to a different condition. Here a turbulence develops which keeps breaking up the bubbles or re-forming them and spreading them apart into a much wider column.”

The nozzle construction and the dimensional characteristics of the installation are described as important features of the invention. A view of the nozzle assembled on a distribution pipe is shown in Fig. 3 of the application reproduced below:

The essence of the application disclosure of the operating characteristics, including dimensions, is as follows:

“ * * * The orifices are of short tubular type, so that they create enough back pressure to help maintain uniformity of flow through the orifices. Four orifices are preferred, partly for ease of drilling the orifices, but even more for certainty of desirable functioning. Four orifices provide fairly good distribution of air through a column of water to provide some air-lift action initially and good air-lift action after the break-up starts. The preferred diameter of the four orifice nozzles is approximately 3", that having been found to be eminently satisfactory. From 1" to 6" is believed to be acceptable, but this should not be taken as implying equal efficiency. The typical orifice diameter found excellent is inch, but from % inch to % inch is believed to be satisfactory. The diameter should be large enough so that there will virtually never be clogging and should be small enough so that the air *980 stream will be small and sufficiently confined, so that water will have no chance of entering an orifice while the air is flowing.
“In a typical, satisfactory operation, sixteen cubic feet of air per minute is liberated through one nozzle (four orifices) with an orifice velocity of 126 ft. per second and with a 7" water column head loss. It is desirable not to let the velocity fall below 70 ft. per second. It then becomes harder to keep the flow balanced through the different nozzles.
“With the usual requirements as to total quantity of air, four orifices of about 5/io inch diameter in each nozzle with the nozzles spaced from 15 inches to 24 inches along the header (or, at the outside 12 inches to 30 inches) has been found to work very satisfactorily.
* * * * *
“The nozzles should be located at a sufficient depth below the liquid level to make sufficient use of the air-lift effect in producing a circulating roll. A submerged depth of about 8 ft. is believed to be about the minimum for efficiency, and 10 ft. or 12 ft. is preferred. The nozzles should be deep enough to cause the circulating roll to move along the bottom of the tank. As with any other type of air liberator for this purpose, excessive depths would require excessive air pressure and pumping costs. For economy, the tank may most efficiently be as wide as can be reliably caused to produce a circulating roll without excessive short-circuiting. * * * ”

Claims 24 and 37 are representative of the appealed claims in P.A. 6772 and read:

“24. A nozzle for introducing gas into a body of liquid comprising a nozzle body having an internal space adapted to be connected to a source of gas under pressure, and a plurality of gas-discharge conduits extending from said internal space, the outlets of said gas-discharging conduits being spaced about a central area of about three inches in diameter, the outlets of said conduits having a transverse dimension of from about one-eighth inch to about three-eights inch and being arranged about said central area at a plurality of points of less than about 180° apart, the outlet ends of said gas-discharge conduits being free of closely-surrounding structure, so that when said nozzle is positioned in a body of liquid and gas discharged from it, the gas will be introduced directly into the liquid and will rise unimpeded in the form of a gas-lift column.
“37. Apparatus for treating a liquid with a gas comprising at least one gas header, nozzles spaced along said gas header, the distance between said nozzles being in excess of about twelve inches, said nozzles having an internal space communicating with said gas header, and gas-discharge conduits extending from said internal space and having outlets spaced about a central area of about three inches in diameter, the outlets of said gas-discharge conduits having a transverse dimension of from about one-eighth inch to about three-eighths inch and being spaced about said central area at points of less than about 180° apart, the outlet ends of said gas-discharge conduits being free of closely-surrounding structure so that when said nozzles are positioned in a body of liquid and gas discharged from them, the gas will be introduced directly into the liquid and will rise unimpeded in the form of a gas-lift column.”

Representative claims on appeal in P.A. 7058 are 9, 23 and 27 which read:

“9. An aeration unit having a fitting at its bottom for communicating with a header, extending up from and communicating with the fitting, having orifice-forming means *981

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Bluebook (online)
324 F.2d 977, 51 C.C.P.A. 954, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-james-donald-walker-two-cases-ccpa-1963.